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2.1.1. Injection through the hole<br />

LES of a bi-periodic turbulent flow with effusion 7<br />

2.1. Generation of a periodic flow with effusion<br />

In experiments, channels are boun<strong>de</strong>d by impermeable walls at the top and at the bottom.<br />

If used in conjunction with periodic boundary conditions in the tangential directions,<br />

this outer condition prevents the flow from reaching a statistically steady state with effusion,<br />

because the n<strong>et</strong> mass flux through the perforation tends to eliminate the pressure<br />

drop b<strong>et</strong>ween the cold and the hot domains. In the present <strong>simulation</strong>s, characteristicbased<br />

freestream boundary conditions (Thompson 1990) are used at the top and bottom<br />

ends of the domain in or<strong>de</strong>r to impose the appropriate mean vertical flow rate. Note that<br />

Men<strong>de</strong>z, Nicoud & Miron (2005) compared this boundary condition-based strategy to<br />

another, source terms-based, m<strong>et</strong>hodology and that the in<strong>de</strong>pen<strong>de</strong>nce of the results on<br />

the m<strong>et</strong>hod used to sustain the effusion was <strong>de</strong>monstrated.<br />

2.1.2. Primary and secondary flows<br />

For classical, periodic channel or pipe flows <strong>simulation</strong>s, a volum<strong>et</strong>ric source term<br />

S (ρ U) is ad<strong>de</strong>d to the streamwise momentum conservation equation in or<strong>de</strong>r to mimic<br />

the effect of the mean streamwise pressure gradient that would exist in a non-periodic<br />

configuration. The source term is constant over space. For example, it can have the<br />

following form:<br />

S (ρ U) = (ρ U targ<strong>et</strong> − ρ U mean )<br />

(2.1)<br />

τ<br />

The source term compares a targ<strong>et</strong> momentum value, ρ U targ<strong>et</strong> , with the spatial-averaged<br />

momentum in the channel, ρ U mean . The time scale τ characterises the relaxation of<br />

ρ U mean towards its targ<strong>et</strong> value. This approach can be generalised to the case of an<br />

effusion configuration, making use of a source term of the previous form in each channel<br />

to generate the primary and the secondary flows and no source term within the hole. Note<br />

however that no source term is required in the aspiration si<strong>de</strong> since the targ<strong>et</strong> velocity<br />

for the secondary flow can be imposed through the boundary condition at the bottom<br />

end of the domain; it is then convected throughout the bottom channel without the need<br />

of extra external forcing.<br />

2.2. Numerical <strong>simulation</strong>s<br />

The smallest domain that can reproduce the geom<strong>et</strong>ry of an infinite plate with staggered<br />

perforations contains only one hole and is diamond-shaped (see figure 2). In the present<br />

isothermal <strong>simulation</strong>s, the computational domain is divi<strong>de</strong>d into two channels. The<br />

upper one, <strong>de</strong>noted by ‘1’, represents the combustion chamber, with a primary flow of<br />

’hot’ gases. The second one, <strong>de</strong>noted by ‘2’, represents the casing, with a secondary flow<br />

of ’cooling’ air. The height of the channels are h 1 = 24 d and h 2 = 10 d respectively,<br />

where d = 5 mm is the diam<strong>et</strong>er of the cylindrical aperture. The upper and lower limits<br />

of the domain are far enough from the zone of interest to avoid any spurious effect of<br />

boundary conditions on the flow near the perforated plate. The channels are separated<br />

by a perforated plate of thickness 10 mm, the aperture being angled at α g = 30 ◦ with<br />

the plate, in the streamwise direction, without any spanwise orientation. The thickness<br />

of the plate being 10 mm and holes being angled at 30 ◦ with the plate, the hole lengthto-diam<strong>et</strong>er<br />

ratio is 4. The diagonals of the computational domain are z = 0 and x = 0<br />

and their lengths equal the hole-to-hole distance, viz. 11.68 d in the streamwise direction<br />

(z = 0) and 6.74 d in the spanwise direction (x = 0). The centre of the hole is located<br />

at x = 0, y = 0, z = 0 for the injection si<strong>de</strong> (hole outl<strong>et</strong>) and at x = −3.46 d, y = −2 d,<br />

z = 0 for the suction si<strong>de</strong> (hole inl<strong>et</strong>).

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